- InChI
- InChI=1S/C2H5I/c1-2-3/h2H2,1H3
- InChI Key
- HVTICUPFWKNHNG-UHFFFAOYSA-N
- Formula
- C2H5I
- SMILES
- CCI
- Molecular Weight1
- 155.97
- CAS
- 75-03-6
- Other Names
-
- 1-Iodoethane
- C2H5I
- ETHYL IODIDE
- Ethyljodid
- HYDRIODIC ETHER
- Iodoethane
- Jodethan
- Monoiodoethane
- NSC 8825
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Rg : Radius of Gyration.
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.1840 | KDB | |
| PAff | 724.80 | kJ/mol | NIST |
| BasG | 698.30 | kJ/mol | NIST |
| ΔcH°liquid | [-1466.00; -1462.50] | kJ/mol |
|
| ΔcH°liquid | -1462.50 ± 0.40 | kJ/mol | NIST |
| ΔcH°liquid | -1466.00 ± 2.00 | kJ/mol | NIST |
| μ | 1.70 | debye | KDB |
| ΔfG° | 21.35 | kJ/mol | KDB |
| Rg | 0.2775 | KDB | |
| ΔfH°gas | [-8.80; -5.40] | kJ/mol |
|
| ΔfH°gas | -8.37 | kJ/mol | KDB |
| ΔfH°gas | -7.20 ± 0.80 | kJ/mol | NIST |
| ΔfH°gas | -8.40 | kJ/mol | NIST |
| ΔfH°gas | -8.80 ± 0.80 | kJ/mol | NIST |
| ΔfH°gas | -5.40 | kJ/mol | NIST |
| ΔfH°liquid | [-39.50; -35.00] | kJ/mol |
|
| ΔfH°liquid | -39.10 ± 0.80 | kJ/mol | NIST |
| ΔfH°liquid | -39.50 ± 1.70 | kJ/mol | NIST |
| ΔfH°liquid | -35.00 | kJ/mol | NIST |
| ΔfusH° | 5.34 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [29.80; 32.05] | kJ/mol |
|
| ΔvapH° | 32.05 | kJ/mol | NIST |
| ΔvapH° | 31.70 | kJ/mol | NIST |
| ΔvapH° | 31.90 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 31.93 ± 0.02 | kJ/mol | NIST |
| ΔvapH° | 29.80 ± 0.30 | kJ/mol | NIST |
| IE | [9.30; 9.60] | eV |
|
| IE | 9.35 ± 0.00 | eV | NIST |
| IE | 9.35 ± 0.00 | eV | NIST |
| IE | 9.33 | eV | NIST |
| IE | 9.33 | eV | NIST |
| IE | 9.30 | eV | NIST |
| IE | 9.35 | eV | NIST |
| IE | 9.35 ± 0.01 | eV | NIST |
| IE | 9.35 ± 0.02 | eV | NIST |
| IE | 9.35 | eV | NIST |
| IE | 9.35 | eV | NIST |
| IE | 9.37 | eV | NIST |
| IE | 9.37 | eV | NIST |
| IE | 9.35 ± 0.02 | eV | NIST |
| IE | 9.33 ± 0.01 | eV | NIST |
| IE | 9.35 ± 0.01 | eV | NIST |
| IE | 9.35 | eV | NIST |
| IE | 9.33 | eV | NIST |
| IE | 9.34 | eV | NIST |
| IE | Outlier 9.60 | eV | NIST |
| IE | 9.45 ± 0.02 | eV | NIST |
| IE | 9.34 | eV | NIST |
| log10WS | [-1.60; -1.60] |
|
|
| log10WS | -1.60 | Aq. Sol... | |
| log10WS | -1.60 | Estimat... | |
| logPoct/wat | 1.441 | Crippen Calculated Property | |
| McVol | 64.860 | ml/mol | McGowan Calculated Property |
| Pc | 4700.00 | kPa | KDB |
| Inp | [586.00; 621.00] |
|
|
| Inp | 614.00 | NIST | |
| Inp | 621.00 | NIST | |
| Inp | 607.00 | NIST | |
| Inp | 586.00 | NIST | |
| Inp | 617.60 | NIST | |
| Inp | 591.00 | NIST | |
| Inp | 598.00 | NIST | |
| Inp | 609.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 616.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 601.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 601.00 | NIST | |
| Inp | 614.00 | NIST | |
| Inp | 591.00 | NIST | |
| Inp | 601.00 | NIST | |
| Inp | 602.00 | NIST | |
| I | [876.00; 901.65] |
|
|
| I | 901.65 | NIST | |
| I | 899.84 | NIST | |
| I | 896.49 | NIST | |
| I | 892.00 | NIST | |
| I | 881.00 | NIST | |
| I | 876.00 | NIST | |
| I | 892.00 | NIST | |
| I | 880.00 | NIST | |
| I | 881.00 | NIST | |
| I | 901.65 | NIST | |
| Tboil | [344.20; 346.35] | K |
|
| Tboil | 345.60 | K | KDB |
| Tboil | 345.50 | K | Isobari... |
| Tboil | Outlier 344.20 | K | NIST |
| Tboil | 345.50 | K | NIST |
| Tboil | 345.60 | K | NIST |
| Tboil | 345.57 ± 0.10 | K | NIST |
| Tboil | 345.45 ± 0.40 | K | NIST |
| Tboil | 346.35 ± 0.30 | K | NIST |
| Tboil | 345.45 ± 0.25 | K | NIST |
| Tboil | 345.50 ± 0.50 | K | NIST |
| Tboil | 345.52 ± 0.25 | K | NIST |
| Tboil | 345.85 ± 0.30 | K | NIST |
| Tboil | 345.50 ± 0.40 | K | NIST |
| Tboil | 345.40 ± 1.00 | K | NIST |
| Tc | 554.00 | K | KDB |
| Tfus | [162.05; 165.00] | K |
|
| Tfus | 165.00 | K | KDB |
| Tfus | 163.62 | K | Aq. Sol... |
| Tfus | 162.05 ± 0.40 | K | NIST |
| Tfus | 162.30 ± 0.40 | K | NIST |
| Vc | 0.235 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [74.51; 98.71] | J/mol×K | [338.30; 544.92] |
|
| Cp,gas | 74.51 | J/mol×K | 338.30 | Joback Calculated Property |
| Cp,gas | 79.14 | J/mol×K | 372.74 | Joback Calculated Property |
| Cp,gas | 83.52 | J/mol×K | 407.17 | Joback Calculated Property |
| Cp,gas | 87.65 | J/mol×K | 441.61 | Joback Calculated Property |
| Cp,gas | 91.55 | J/mol×K | 476.05 | Joback Calculated Property |
| Cp,gas | 95.23 | J/mol×K | 510.48 | Joback Calculated Property |
| Cp,gas | 98.71 | J/mol×K | 544.92 | Joback Calculated Property |
| Cp,liquid | [109.70; 115.10] | J/mol×K | [298.00; 298.15] |
|
| Cp,liquid | 115.10 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 109.70 | J/mol×K | 298.15 | NIST |
| η | [0.0004224; 0.0050904] | Pa×s | [170.36; 338.30] |
|
| η | 0.0050904 | Pa×s | 170.36 | Joback Calculated Property |
| η | 0.0025088 | Pa×s | 198.35 | Joback Calculated Property |
| η | 0.0014730 | Pa×s | 226.34 | Joback Calculated Property |
| η | 0.0009723 | Pa×s | 254.33 | Joback Calculated Property |
| η | 0.0006970 | Pa×s | 282.32 | Joback Calculated Property |
| η | 0.0005305 | Pa×s | 310.31 | Joback Calculated Property |
| η | 0.0004224 | Pa×s | 338.30 | Joback Calculated Property |
| ΔvapH | [29.44; 34.70] | kJ/mol | [273.50; 345.60] |
|
| ΔvapH | 32.00 | kJ/mol | 273.50 | NIST |
| ΔvapH | 34.70 | kJ/mol | 282.00 | NIST |
| ΔvapH | 33.60 | kJ/mol | 309.00 | NIST |
| ΔvapH | 31.70 | kJ/mol | 318.00 | NIST |
| ΔvapH | 29.77 | kJ/mol | 345.60 | KDB |
| ΔvapH | 29.44 | kJ/mol | 345.60 | NIST |
| Pvap | 101.30 | kPa | 345.50 | Isobari... |
| n0 | 1.50950 | 298.15 | Experim... | |
| ρl | [1923.80; 1950.00] | kg/m3 | [293.00; 298.15] |
|
| ρl | 1950.00 | kg/m3 | 293.00 | KDB |
| ρl | 1923.80 | kg/m3 | 298.15 | Solubil... |
| γ | 0.03 | N/m | 293.20 | KDB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [251.46; 368.73] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.45544e+01 | |||
| Coefficient B | -3.07804e+03 | |||
| Coefficient C | -3.57160e+01 | |||
| Temperature range, min. | 251.46 | |||
| Temperature range, max. | 368.73 | |||
| Pvap | 1.33 | kPa | 251.46 | Calculated Property |
| Pvap | 3.00 | kPa | 264.49 | Calculated Property |
| Pvap | 6.20 | kPa | 277.52 | Calculated Property |
| Pvap | 11.89 | kPa | 290.55 | Calculated Property |
| Pvap | 21.40 | kPa | 303.58 | Calculated Property |
| Pvap | 36.47 | kPa | 316.61 | Calculated Property |
| Pvap | 59.27 | kPa | 329.64 | Calculated Property |
| Pvap | 92.45 | kPa | 342.67 | Calculated Property |
| Pvap | 139.08 | kPa | 355.70 | Calculated Property |
| Pvap | 202.64 | kPa | 368.73 | Calculated Property |
| Pvap | [1.10e-04; 5970.39] | kPa | [162.05; 561.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.81996e+01 | |||
| Coefficient B | -5.85116e+03 | |||
| Coefficient C | -8.13893e+00 | |||
| Coefficient D | 7.75920e-06 | |||
| Temperature range, min. | 162.05 | |||
| Temperature range, max. | 561.00 | |||
| Pvap | 1.10e-04 | kPa | 162.05 | Calculated Property |
| Pvap | 0.04 | kPa | 206.38 | Calculated Property |
| Pvap | 1.47 | kPa | 250.71 | Calculated Property |
| Pvap | 15.74 | kPa | 295.03 | Calculated Property |
| Pvap | 83.55 | kPa | 339.36 | Calculated Property |
| Pvap | 289.13 | kPa | 383.69 | Calculated Property |
| Pvap | 761.73 | kPa | 428.02 | Calculated Property |
| Pvap | 1679.28 | kPa | 472.34 | Calculated Property |
| Pvap | 3291.20 | kPa | 516.67 | Calculated Property |
| Pvap | 5970.39 | kPa | 561.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Ethane, iodo-.
Mixtures
- Toluene + Ethane, iodo-
- Ethane, iodo- + Methyl Alcohol
- Ethane, iodo- + Ethanol
- 1-Propanol + Ethane, iodo-
- Toluene + Ethane, iodo- + Methyl Alcohol
- Toluene + Ethane, iodo- + Ethanol
- 1-Propanol + Toluene + Ethane, iodo-
- Ethane, iodo- + Propanoic acid
- Propanoic acid, ethyl ester + Ethane, iodo-
- Ethane, iodo- + Methyl Alcohol + Water
- Ethane, iodo- + Ethanol + Water
- 1-Propanol + Ethane, iodo- + Water
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Experimental and predicted volumetric and refractive index properties of ternary mixtures of iodoethane with toluene and alcohols at temperature 298.15 K and pressure 101 kPa
- Isobaric vapour-liquid equilibrium for binary systems of ethyl iodide with ethanol, propionic acid and ethyl propionate at 101.3 kPa
- Solubility and Liquid-Liquid Equilibrium of Aqueous Systems of Iodoethane with Methanol, Ethanol, or 1-Propanol at Temperature 298.15 K and Pressure 101.2 kPa
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.